CN112028340A - High-efficient separator - Google Patents

High-efficient separator Download PDF

Info

Publication number
CN112028340A
CN112028340A CN202011022136.4A CN202011022136A CN112028340A CN 112028340 A CN112028340 A CN 112028340A CN 202011022136 A CN202011022136 A CN 202011022136A CN 112028340 A CN112028340 A CN 112028340A
Authority
CN
China
Prior art keywords
water
sludge
pipe
flaring
filter
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN202011022136.4A
Other languages
Chinese (zh)
Inventor
罗礼朋
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to CN202011022136.4A priority Critical patent/CN112028340A/en
Publication of CN112028340A publication Critical patent/CN112028340A/en
Pending legal-status Critical Current

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/52Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/001Processes for the treatment of water whereby the filtration technique is of importance
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00Specific treatment goals
    • C02F2303/16Regeneration of sorbents, filters

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Treatment Of Sludge (AREA)

Abstract

The invention discloses a high-efficiency separation device, which comprises a solid-liquid separation device, wherein the solid-liquid separation device is sequentially provided with a first guide pipe, a first flaring, a second guide pipe and a second flaring which are communicated from bottom to top, the first guide pipe is provided with a water inlet arranged along the tangential direction, the first guide pipe is internally provided with a water flow rotating guide device for receiving sewage entering from the water inlet, the second flaring is internally provided with a sludge recovery cylinder, a muddy water rising channel is formed between the sludge recovery cylinder and the second flaring, and the sludge recovery cylinder is provided with a sludge discharge pipe which passes through the second flaring and is communicated with the outside. After flocculation treatment, sewage enters the first conduit from the water inlet in a tangential direction to generate rotary motion, and the water flow rotary guide device guides the rotary water flow to spirally rise. When sewage reaches the top of the second flaring through the muddy water ascending channel, large-particle sludge formed after flocculation is continuously settled under the action of gravity to form a sludge filtering layer so as to intercept sludge with a certain particle size and achieve the effect of efficient filtering.

Description

High-efficient separator
Technical Field
The invention is used in the technical field of sewage purification, and particularly relates to a high-efficiency separation device.
Background
At present, in the sewage treatment process, in order to treat sewage and meet certain discharge or recycling requirements, a sewage filtering device is required to be adopted to filter the sewage. The sewage filtering device in the prior art is composed of a shell, a water inlet pipe, a water outlet pipe and a filtering chamber, wherein the filtering chamber adopts an upper inlet and lower outlet mode, sewage is sent into the filtering chamber from a water inlet pipe at the top, and the sewage is filtered by a filter material in the filtering chamber and then discharged from a water outlet pipe at the bottom to reach the standard. The sewage filtration performed in this way has the following disadvantages: the filter material is deposited, and the filter material is not easy to clean during back washing, so that the sewage filtering effect is poor, and the filtering efficiency is low.
Disclosure of Invention
The invention aims to at least solve one of the technical problems in the prior art, and provides a high-efficiency separation device which adopts a mode of feeding sewage downwards and discharging clean water upwards, and utilizes a sludge filter layer generated by mud-water separation as a filter medium to improve the filtering effect and the filtering efficiency.
The technical scheme adopted by the invention for solving the technical problems is as follows:
the utility model provides a high-efficient separator, includes solid-liquid separation equipment, solid-liquid separation equipment is from up being equipped with the first pipe, first flaring, second pipe and the second flaring that are linked together down in proper order, be equipped with the water inlet that sets up along tangential direction on the first pipe, be equipped with the rotatory guider of rivers in the first pipe, in order to receive the follow the sewage that the water inlet got into, be equipped with sludge recycling bin in the second flaring, sludge recycling bin with form muddy water ascending passageway between the second flaring, be equipped with on the sludge recycling bin and pass the second flaring and with the mud contact tube of outside intercommunication.
In combination with the above implementation manners, in some implementation manners of the present invention, the present invention further includes a tank, the solid-liquid separation device is located in the tank, the second flared opening abuts against an inner wall of the tank, and divides the tank into a sludge storage chamber and a filter chamber, the sludge storage chamber is located below the filter chamber, the sludge discharge pipe passes through the second flared opening and then communicates with the sludge storage chamber, the tank is provided with a communicating pipe communicating with the sludge storage chamber, the bottom of the tank is provided with a sludge discharge port communicating with the sludge storage chamber, and the top of the tank is provided with a water outlet.
With reference to the foregoing implementation manners, in some implementation manners of the present invention, a suspended filter material is disposed in the filter cavity, and a filter material intercepting component is disposed at the top of the filter cavity.
With reference to the foregoing implementation manners, in some implementation manners of the present invention, the tank is provided with a first filtering component above the filter material intercepting component, the first filtering component is provided with a plurality of first filtering caps, the tank forms a standard reaching clear water cavity above the first filtering component, and the water outlet is communicated with the standard reaching clear water cavity.
With reference to the foregoing implementation manners, in some implementation manners of the present invention, both ends of the communication pipe are communicated with the sludge storage chamber, the communication pipe passes around the filter chamber, the filter chamber of the communication pipe is provided with a plurality of third filter caps distributed along the length, a cap handle of each third filter cap is communicated with the communication pipe, both ends of the communication pipe are provided with the first valves, and the communication pipe is provided with the first water openings.
With reference to the foregoing implementation manners, in some implementation manners of the present invention, a filter material backwashing device is further disposed in the filter cavity, and the filter material backwashing device includes an annular water through pipe and a plurality of water distribution pipes, the water distribution pipes are circumferentially distributed at intervals in the annular water through pipe, the water distribution pipes are provided with first flushing ports, and the annular water through pipe is provided with second water through ports.
With reference to the foregoing implementation manners, in some implementation manners of the present invention, a sludge cleaning pipe is disposed in the sludge storage cavity, a plurality of second flushing ports are disposed on the sludge cleaning pipe at intervals, a third water passage port is disposed on the sludge cleaning pipe, and the first water passage port, the second water passage port, and the third water passage port are all connected to the water conduit through a second valve.
With reference to the foregoing implementation manners, in some implementation manners of the present invention, a second filtering component is disposed on the second flared opening, and a plurality of second filtering caps are disposed on the second filtering component.
With reference to the foregoing implementation manners, in some implementation manners of the present invention, the present invention further includes a water inlet pump and a chemical reaction device, the chemical reaction device is used for placing a sewage treatment agent, the water inlet pump is used for pumping muddy water into the chemical reaction device, the chemical reaction device is connected with the water inlet through a water inlet pipe, and a third valve is disposed on the water inlet pipe.
In combination with the above implementations, in certain implementations of the invention, the water flow rotating guide includes a helical blade.
One of the above technical solutions has at least one of the following advantages or beneficial effects: when sewage is filtered, sewage enters the first conduit from the water inlet in a tangential direction after being subjected to flocculation treatment, so that the sewage generates rotary motion in the first conduit, and the water flow rotary guide device guides the rotary water flow to spirally rise. When sewage passes through the first flaring and the second flaring, the flow velocity of the sewage is reduced, and the sewage reaches the top of the second flaring through the muddy water ascending channel under the centrifugal action, at the moment, large-particle sludge formed after flocculation is continuously settled under the action of gravity to form a sludge filtering layer so as to intercept sludge with a certain particle size, and the filtering effect is achieved. In addition, through mud delivery pipe pressure release, arouse to produce the vortex in the sludge recycling bin to inhale the mud of the mud filter layer on the second flaring in the sludge recycling bin, and discharge along mud delivery pipe, reach the effect of discharging clear water on the mud down, improve filter effect and filtration efficiency.
Drawings
The invention will be further described with reference to the accompanying drawings in which:
FIG. 1 is a schematic block diagram of one embodiment of the present invention;
FIG. 2 is a schematic structural view of a tank and a solid-liquid separation device according to one embodiment shown in FIG. 1;
FIG. 3 is a schematic top view of the solid-liquid separation device and second filter element of one embodiment shown in FIG. 1;
FIG. 4 is a schematic top view of the filter material backwash assembly of one embodiment of FIG. 1.
Detailed Description
Reference will now be made in detail to the present preferred embodiments of the present invention, examples of which are illustrated in the accompanying drawings, wherein like reference numerals refer to like elements throughout.
In the present invention, if directions (up, down, left, right, front, and rear) are described, it is only for convenience of describing the technical solution of the present invention, and it is not intended or implied that the technical features referred to must have a specific orientation, be constructed and operated in a specific orientation, and thus, it is not to be construed as limiting the present invention.
In the invention, the meaning of "a plurality" is one or more, the meaning of "a plurality" is more than two, and the terms of "more than", "less than", "more than" and the like are understood to exclude the number; the terms "above", "below", "within" and the like are understood to include the instant numbers. In the description of the present invention, if there is description of "first" and "second" only for the purpose of distinguishing technical features, it is not to be understood as indicating or implying relative importance or implicitly indicating the number of indicated technical features or implicitly indicating the precedence of the indicated technical features.
In the present invention, unless otherwise specifically limited, the terms "disposed," "mounted," "connected," and the like are to be understood in a broad sense, and for example, may be directly connected or indirectly connected through an intermediate; can be fixedly connected, can also be detachably connected and can also be integrally formed; may be mechanically coupled, may be electrically coupled or may be capable of communicating with each other; either as communication within the two elements or as an interactive relationship of the two elements. The specific meaning of the above-mentioned words in the present invention can be reasonably determined by those skilled in the art in combination with the detailed contents of the technical solutions.
Referring to fig. 1 and 2, an embodiment of the present invention provides an efficient separation device, which includes a solid-liquid separation device, the solid-liquid separation device is sequentially provided with a first conduit 11, a first flared opening 12, a second conduit 13, and a second flared opening 14, which are communicated with each other, from bottom to top, the first conduit 11 is provided with a water inlet 111 arranged along a tangential direction, so that sewage can form a rotational water flow when entering from the water inlet 111. The first guide pipe 11 is provided therein with a water flow rotation guide 112 to receive the sewage entering from the water inlet 111 and to guide the sewage rotating at a high speed to move upward in a spiral ascending manner. Under the guidance of the water flow rotating guide device 112, sewage is subjected to first speed reduction from the first guide pipe 11 through the first flaring 12 and then enters the second flaring 14 from the second guide pipe 13 for second speed reduction, so that when muddy water reaches the top of the second flaring 14, large-particle sludge can be gradually settled to form a sludge filtering layer.
Referring to fig. 2, a sludge recovery cylinder 141 is disposed in the second flared end 14, and a sludge water ascending channel 142 is formed between the sludge recovery cylinder 141 and the second flared end 14. The muddy water can only be decelerated and ascended from the muddy water ascending channel 142 in the second flaring 14 due to the centrifugal force during the spiral ascending. The sludge recycling cylinder 141 is provided with a sludge leading-out pipe 143 which penetrates through the second flaring 14 and is communicated with the outside, and the sludge leading-out pipe 143 can be communicated with the outside, so that when the sludge recycling cylinder 141 is decompressed through the sludge leading-out pipe 143 to generate a vortex, sludge in a sludge filtering layer at the top of the second flaring 14 is acted by centripetal force, is sucked into the sludge recycling cylinder 141 and is discharged through the sludge leading-out pipe 143.
When the sewage is filtered, the sewage enters the first conduit 11 tangentially from the water inlet 111 after being subjected to flocculation treatment, so that the sewage generates rotary motion in the first conduit 11, and the water flow rotary guide device 112 guides the rotary water flow to spirally rise. When sewage passes through the first flaring 12 and the second flaring 14, the flow rate of the sewage is reduced, and the sewage reaches the top of the second flaring 14 through the muddy water ascending channel 142 under the centrifugal action, at the moment, large-particle sludge formed after flocculation is continuously settled under the action of gravity to form the sludge filtering layer 2 so as to intercept sludge with a certain particle size, and the filtering effect is achieved. In addition, the pressure is released through the sludge leading-out pipe 143, which causes vortex flow to be generated in the sludge recycling cylinder 141, so that the sludge of the sludge filtering layer 2 on the second flaring 14 is sucked into the sludge recycling cylinder 141 and discharged along the sludge leading-out pipe 143, and the effect of discharging clean water on the lower row of sludge is achieved. The sludge filtering layer 2 is continuously formed on the second flared end 14, and simultaneously, the sludge can be discharged from the sludge recovery cylinder 141, so that dynamic balance is formed. According to the technical scheme, sludge generated by mud-water separation is used as a filtering medium, so that the environment is protected, the energy is saved, the purpose of efficiently filtering sewage is achieved, and the filtering effect and the filtering efficiency are improved.
Referring to fig. 1 and 2, in some embodiments, the high-efficiency separation device further comprises a tank body 3, the solid-liquid separation device is positioned in the tank body 3, and the second flaring 14 abuts against the inner wall of the tank body 3 and divides the tank body 3 into a sludge storage cavity 31 and a filter cavity 32. The sludge storage cavity 31 is positioned below the filter cavity 32, and the sludge delivery pipe 143 passes through the second flaring 14 and then is communicated with the sludge storage cavity 31. More specifically, the sludge recovery cylinder 141 has a tapered shape, and the sludge outlet pipe 143 obliquely passes through the second enlarged opening 14, so that the space of the sludge-water rising passage 142 can be increased by providing the sludge recovery cylinder 141 with a tapered shape, thereby improving the filtering efficiency. Referring to fig. 2, the tank 3 is provided with a communicating pipe 33 communicating with the sludge storage chamber 31, and when the communicating pipe 33 is opened, the inside of the sludge storage chamber 31 is depressurized, thereby forming a vortex in the sludge recovery drum 141. The bottom of the tank 3 is provided with a sludge discharge port 311 communicating with the sludge storage chamber 31. When the sludge is discharged through the sludge discharge pipe 143, the sludge falls into the sludge storage chamber 31 and is discharged out of the high-efficiency separation device through the sludge discharge port 311. A water outlet 34 is arranged at the top of the tank body 3, and the filtered clean water is discharged out of the tank body 3 through the water outlet 34.
Referring to fig. 1 and 2, in some embodiments, the filter chamber 32 is provided with a suspended filter material 4 therein, and the top of the filter chamber 32 is provided with a filter material intercepting component 321, which plays a role of intercepting the suspended filter material 4. After the mud water rises along the solid-liquid separation device and is filtered by the sludge filter layer 2, the mud water with the small-particle sludge continuously rises and fills the filter cavity 32, so that the suspended filter material 4 in the filter cavity 32 is suspended and cannot continuously rise under the action of the filter material intercepting component 321. At this time, the muddy water filtered by the sludge filter layer 2 is filtered again by the suspended filter material 4 in the process of rising, and the sewage filtering effect is improved.
Referring to fig. 2, in some embodiments, the first filter element 35 is disposed above the filter material intercepting element 321 of the tank 3, and the first filter element 35 is provided with a plurality of first filter caps 351, so as to filter relatively clean water rising above the filter material intercepting element 321 again, thereby meeting the requirement of sewage treatment. The tank body 3 is provided with a standard reaching clear water cavity 36 above the first filtering component 35, and the water outlet 34 is communicated with the standard reaching clear water cavity 36. The water filtered by the first filtering component 35 can become clear water reaching the standard, and the clear water reaching the standard flows into the water outlet 34 through the clear water cavity 36 reaching the standard and finally flows out of the tank body 3.
Referring to fig. 2 and 3, in some embodiments, a second filtering member 144 is disposed on the second flared end 14, and a plurality of second filtering caps 145 are disposed on the second filtering member 144 to filter the muddy water rising into the second flared end 14 for the first time to remove larger particles of sludge.
The communicating pipe 33 can be directly connected to the outside of the tank 3 or connected to the filter chamber 32 after communicating with the sludge storage chamber 31. Referring to fig. 1 and 2, in some embodiments, both ends of the communication pipe 33 are communicated with the sludge storage chamber 31, the communication pipe 33 passes around the filter chamber 32, the communication pipe 33 is provided with a plurality of third filter caps 331 distributed along the length in the filter chamber 32, a cap handle of the third filter cap 331 is communicated with the communication pipe 33, both ends of the communication pipe 33 are provided with first valves 332, and the communication pipe 33 is provided with first water ports. When the sewage filtering and the filter material backwashing are stopped, the first valve 332 is closed, external water flows into the communicating pipe 33 through the first water passage port and flows out from the third filter cap 331 to flush the filter material, so that the flushed water sequentially passes through the filter chamber 32, the second flaring 14 of the solid-liquid separation device or the sludge recovery drum 141, and finally flows out from the sludge discharge port 311 through the sludge storage chamber 31. When the muddy water is filtered, the first water through port is closed, and the first valve 332 is opened to release the pressure of the sludge storage cavity 31.
Referring to fig. 2 and 4, in some embodiments, the filter chamber 32 further includes a filter material backwashing device, which includes an annular water pipe 51 and a plurality of water distribution pipes 52, the water distribution pipes 52 are circumferentially spaced apart from the annular water pipe 51, the water distribution pipes 52 are provided with first flushing ports, and the annular water pipe 51 is provided with second flushing ports. When the filter material is backwashed, water enters the annular water through pipe 51 through the second water through port and finally flows out through the water distribution pipe 52 to backwash the filter material.
Referring to fig. 1 and 2, in some embodiments, a sludge cleaning pipe 312 is disposed in the sludge storage chamber 31, and a plurality of second flushing ports are disposed on the sludge cleaning pipe 312 at intervals to flush the sludge storage chamber 31. The sludge cleaning pipe 312 is provided with a third water through opening, and the first water through opening, the second water through opening and the third water through opening are all connected with the water conduit 61 through a second valve 6. During back flushing, the second valves 6 at the first water through port, the second water through port and the third water through port are opened respectively, and water can flow to the third filter cap 331, the first flushing port and the second flushing port respectively to perform flushing operation.
Referring to fig. 1, in some embodiments, the high efficiency separation apparatus further comprises a water inlet pump 71 and a chemical reaction apparatus 72, wherein the chemical reaction apparatus 72 is used for placing sewage treatment agent. The water inlet pump 71 is used for pumping muddy water into the chemical reaction device 72, and the muddy water can flocculate larger granular sludge after being added with the sewage treatment agent. The chemical reaction device 72 is connected with the water inlet 111 through a water inlet pipe 73, the water inlet pipe 73 is provided with a third valve 74, and the flow rate, the pressure and the like of the sewage are controlled through the third valve 74. Wherein, the sewage treatment agent can adopt flocculating agent, coagulant aid, coagulant and the like.
In some embodiments, the water flow rotating guide 112 includes helical blades on which the rotating water flow formed by the tangentially entering contaminated water acts, and which guide the water flow upward in a spiral ascending manner.
When the efficient separation device of the technical scheme is used for purifying sewage, the sewage after flocculation treatment is tangentially sent into the first guide pipe 11 to form rotary water flow, the rotary water flow spirally rises under the action of the spiral blades and sequentially passes through the first flaring openings 12 and the second flaring openings 14 to reduce the speed of rising of muddy water, so that large-particle sludge can gradually settle to form the sludge filter layer 2 when reaching the upper part of the second flaring openings 14. Wherein, the second filtering part 144 can filter the muddy water for the first time when the muddy water passes through the muddy water rising channel 142 of the second flaring 14; when the muddy water rises to the sludge filtering layer 2, the muddy water can be filtered for the second time by the sludge filtering layer 2; the muddy water continuously rises to the filter cavity 32, is filtered for the third time by the suspension filter material 4, finally rises to the first filter component 35 through the filter cavity 32, is filtered for the fourth time by the first filter component 35 to reach the clear water standard, enters the standard clear water cavity 36, and is finally discharged from the water outlet 34, so that the filter effect and the filter efficiency are ensured, and the environmental protection performance is improved.
In the description herein, references to the description of the term "example," "an embodiment," or "some embodiments," etc., mean that a particular feature, structure, material, or characteristic described in connection with the embodiment or example is included in at least one embodiment or example of the invention. In this specification, the schematic representations of the terms used above do not necessarily refer to the same embodiment or example. Furthermore, the particular features, structures, materials, or characteristics described may be combined in any suitable manner in any one or more embodiments or examples.
The invention is not limited to the above embodiments, and those skilled in the art can make equivalent modifications or substitutions without departing from the spirit of the invention, and such equivalent modifications or substitutions are included in the scope defined by the claims of the present application.

Claims (10)

1. An efficient separation device is characterized in that: including solid-liquid separation equipment, solid-liquid separation equipment is from up being equipped with the first pipe, first flaring, second pipe and the second flaring that are linked together in proper order down, be equipped with the water inlet that sets up along tangential direction on the first pipe, be equipped with the rotatory guider of rivers in the first pipe, in order to receive the follow the sewage that the water inlet got into, be equipped with sludge recycling cylinder in the second flaring, sludge recycling cylinder with form the ascending passageway of muddy water between the second flaring, be equipped with on the sludge recycling cylinder and pass the second flaring and with the mud contact tube of outside intercommunication.
2. The high efficiency separation device of claim 1, wherein: still include a jar body, solid-liquid separation equipment is located in the jar body, the second flaring supports the inner wall of the jar body, and will the jar body is separated into mud storage chamber and filter chamber, mud storage chamber is located the below of filter chamber, the mud contact tube passes behind the second flaring with mud storage chamber intercommunication, the jar body be equipped with the communicating pipe of mud storage chamber intercommunication, the bottom of the jar body be equipped with the mud discharge port of mud storage chamber intercommunication, the top of the jar body is equipped with the delivery port.
3. The high efficiency separation device of claim 2, wherein: the filter cavity is internally provided with a suspended filter material, and the top of the filter cavity is provided with a filter material intercepting component.
4. A high efficiency separation device as claimed in claim 3, wherein: the tank body is provided with a first filter element above the filter material interception element, the first filter element is provided with a plurality of first filter caps, the tank body is provided with a standard reaching clear water cavity above the first filter element, and the water outlet is communicated with the standard reaching clear water cavity.
5. The high efficiency separation device of claim 2, wherein: the two ends of the communicating pipe are communicated with the sludge storage cavity, the communicating pipe is wound through the filter cavity, the communicating pipe is arranged in the filter cavity and provided with a plurality of third filter caps distributed along the length, a cap handle of each third filter cap is communicated with the communicating pipe, the two ends of the communicating pipe are provided with first valves, and each communicating pipe is provided with a first water through port.
6. The high efficiency separation device of claim 5, wherein: the filter cavity is also internally provided with a filter material backwashing device, the filter material backwashing device comprises an annular water through pipe and a plurality of water distribution pipes, the water distribution pipes are circumferentially distributed on the annular water through pipe at intervals, the water distribution pipes are provided with first flushing ports, and the annular water through pipe is provided with second water through ports.
7. The high efficiency separation device of claim 6, wherein: the sludge storage cavity is internally provided with a sludge cleaning pipe, the sludge cleaning pipe is provided with a plurality of second flushing ports distributed at intervals, the sludge cleaning pipe is provided with a third water through port, and the first water through port, the second water through port and the third water through port are all connected with a water guide pipe through a second valve.
8. The high efficiency separation device of claim 1, wherein: and a second filtering component is arranged on the second flaring, and a plurality of second filtering caps are arranged on the second filtering component.
9. The high efficiency separation device of claim 1, wherein: still include intake pump and chemical reaction unit, chemical reaction unit is used for putting into sewage treatment medicament, the intake pump is used for with muddy water pump income among the chemical reaction unit, chemical reaction unit pass through the inlet tube with the water inlet is connected, be equipped with the third valve on the inlet tube.
10. The high efficiency separation device of claim 1, wherein: the water flow rotating and guiding device comprises a spiral blade.
CN202011022136.4A 2020-09-25 2020-09-25 High-efficient separator Pending CN112028340A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202011022136.4A CN112028340A (en) 2020-09-25 2020-09-25 High-efficient separator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202011022136.4A CN112028340A (en) 2020-09-25 2020-09-25 High-efficient separator

Publications (1)

Publication Number Publication Date
CN112028340A true CN112028340A (en) 2020-12-04

Family

ID=73575244

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202011022136.4A Pending CN112028340A (en) 2020-09-25 2020-09-25 High-efficient separator

Country Status (1)

Country Link
CN (1) CN112028340A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113041709A (en) * 2021-03-12 2021-06-29 中国恩菲工程技术有限公司 Filtration system and method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113041709A (en) * 2021-03-12 2021-06-29 中国恩菲工程技术有限公司 Filtration system and method

Similar Documents

Publication Publication Date Title
CN212356858U (en) High-efficient separator
CN201330186Y (en) High-efficiency integrated water purifying apparatus with helical sloping plate
CN107235569A (en) A kind of hydraulic engineering mud wastewater treatment equipment
CN105413284A (en) Liquid filtering method and filtering device
CN108525353A (en) A kind of settling tank efficiently separated
CN201567272U (en) Sewage purifier
CN108124430B (en) Vortex solid-liquid separator
CN112028340A (en) High-efficient separator
CN202146667U (en) Backwash type pre-filter
CN209940659U (en) High-efficient multistage flocculation and precipitation all-in-one device
CN216639004U (en) Self-circulation encrypted granular sludge water purifying device
CN110104838A (en) A kind of the AUTOMATIC ZONING separating treatment system and its processing method of oily wastewater
CN208177056U (en) A kind of trade effluent filter
CN206219359U (en) Pollutant-removing system
CN111617520B (en) Turbulent flow sedimentation tank
CN209778423U (en) high-efficiency flocculation sedimentation water purification equipment
CN107226562A (en) A kind of chemical industry purifying sewage quickly device
CN212504362U (en) Reaction precipitator for water purification
CN113968639B (en) Self-circulation high-density suspended sludge filtering and sedimentation water purifying device
CN214019538U (en) Liquid filtering device
CN215480210U (en) Self-circulation high-density suspended sludge filtering and settling water purifying device
CN214936462U (en) Waste water recovery system of thermal power plant
CN214936565U (en) Grid grit chamber for treating domestic sewage
CN213221280U (en) Negative pressure sewage filtration treatment device
CN113856591B (en) High-efficient concentration reaction kettle

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination